A drying system for drying an agriculture product is disclosed. The drying system includes an enclosure having one or more wall structures and defining a chamber for receiving and storing the agricultural product. Each wall structure includes an inner wall having a plurality of wood panels and an outer wall. Each wood panel is a treated wood panel and is adapted to absorb moisture from an air circulating inside the chamber. Each wood panel is treated with a solution of calcium chloride to enhance a moisture absorbing capacity. The outer wall is disposed substantially parallel and spaced apart from the inner wall and defines a gap therebetween. The enclosure further includes one or more moisture absorbing materials disposed inside the gap to absorb moisture received from the inner wall.

Method for the preparation of dried polymer pellets in a facility having a dryer with a first chamber and a mechanical agitator, and the facility further having a degassing silo with a second chamber, the method includes the steps of guiding a drying gas flow made from or containing a first gas mixture for drying wet polymer pellets into the first chamber, transferring the dried polymer pellets into the second chamber, guiding a second gas mixture for degassing the dried polymer pellets into the second chamber thereby transforming the second gas mixture into a third gas mixture and guiding a portion of the third gas mixture into the first chamber; and process for manufacturing LDPE pellets.

A method of drying soft capsules including steps of: a) supplying a flow of air to said soft capsules at a velocity of the air across the soft capsules of from about 0.15 m/s to about 13 m/s; b) increasing, over time, a drying temperature to which said soft capsules are exposed while ensuring that the drying temperature remains below a melting temperature of a capsule shell of the soft capsules; c) exposing said soft capsules to an initial relative humidity of from about 49% RH to about 79% RH; d) decreasing the relative humidity to which the soft capsules are exposed as the capsules dry until an equilibrium relative humidity of the soft capsules reaches a desired relative humidity; and e) exposing the soft capsules from step d) to a temperature of from 20-25° C. Also disclosed is a drying system for carrying out the method.

The present invention provides a hay bale dryer, comprising: a platform, the platform dimensioned to support the hay bale; a spike rack movably coupled to the platform, the spike rack having a plurality of spikes, each spike having a plurality of slots and each spike dimensioned to penetrate through the hay bale; a fan coupled to the spike rack and operative to blow air through the slots in the spikes, wherein the spike rack is raised to permit loading and unloading of the hay bale, and lowered to permit drying of the hay bale via the air blown through the spikes.

Methods and apparatuses for drying web substrates are described. In one embodiment, a method of drying a web substrate may comprise supplying air to a first dryer head located proximate a web conveyer, the air within the first dryer head having a temperature of less than 176 degrees C., directing air from the first dryer head toward the web conveyer at a velocity greater than 1000 m/min and forming a first drying region, and advancing the web substrate in a first direction on the web conveyer and through the first drying region.

Methods and apparatuses for drying web substrates are described. In one embodiment, a method of drying a web substrate may comprise supplying air to a first dryer head located proximate a web conveyer, the air within the first dryer head having a temperature of less than 176 degrees C., directing air from the first dryer head toward the web conveyer at a velocity greater than 1000 m/min and forming a first drying region, and advancing the web substrate in a first direction on the web conveyer and through the first drying region.

A system for supporting and drying personal protective equipment includes a ducting frame assembly, ventilated equipment racks connected to the frame assembly, and valves between the equipment racks and the ducting frame assembly. The system is supported by a base assembly, bracing, or a combination of a base and braces. A blower forces air through the frame assembly and may heat the air and add disinfecting or deodorizing substances to the air flow. Valves may be opened to direct the forced air into equipment racks and through ventilation apertures or openings in the racks. Personal protective equipment may be disposed upon the equipment racks, so that air is ventilated out of the racks and onto and around protective equipment on the racks.

The present disclosure provides a surface cleaning apparatus that includes a recovery system that extracts liquid and debris with a drying cycle in which forced air flows through a recovery pathway of the recovery system to dry out components that remain wet and/or retain moisture after normal operation of the apparatus. The post-operation drying cycle can dry out components such as an agitator or brushroll, a brush chamber, a suction nozzle, a recovery tank, a filter, and any of the various conduits, ducts, and/or hoses fluidly coupling components of the recovery system together.

The present invention relates to a system for one pot solids recovery from solutions, slurries, emulsions, dispersions, gels, semisolids, and their like. Further the system can be used for controlled concentration of solutions, slurries, emulsions, dispersions, gels, semisolids, and their like to enable easy to operate cost effective energy efficient processes. The system is so constructed to enhance the contact between the liquid medium and the gaseous medium used in the process for effective heat transfer. The system can be used for controlled concentration and/or recovery of substantially dry solids in applications related to foods, nutraceuticals, natural products, pharmaceuticals, chemicals, etc.

The present invention relates to a system for one pot solids recovery from solutions, slurries, emulsions, dispersions, gels, semisolids, and their like. Further the system can be used for controlled concentration of solutions, slurries, emulsions, dispersions, gels, semisolids, and their like to enable easy to operate cost effective energy efficient processes. The system is so constructed to enhance the contact between the liquid medium and the gaseous medium used in the process for effective heat transfer. The system can be used for controlled concentration and/or recovery of substantially dry solids in applications related to foods, nutraceuticals, natural products, pharmaceuticals, chemicals, etc.